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US4352915A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the polymerization of ethylene

Assignee: Sumitomo Chemical Co Ltd
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Filing: 1980-05-23
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Granted: 1982-10-05
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Expires: 2000-05-23
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Abstract

Abstract In a slurry polymerization for producing an ethylene homopolymer or ethylene-α-olefin copolymer in multiple stages, in which the gas phase hydrogen concentration in each stage is different, using a catalyst system comprising a transition metal compound component and an organoaluminum compound component, the improvement which comprises conducting the polymerization by the use of a solid catalyst component comprising a titanium compound and/or vanadium compound supported on a specified magnesium compound, as the transition metal compound component, in a molar ratio of gas phase hydrogen to ethylene of 0.5 to 15 in the first stage thereby obtaining 30 to 95% by weight, of the total polymer, and in the second stage in a molar ratio of gas phase hydrogen to ethylene, not exceeding 0.2. By this process, it is possible to produce polyethylene having high melt flow and good homogeneity to give molded articles having fewer fish-eyes and less unevenness.

Inventors

  • 👤 Kentaro Mashita
  • 👤 Katsumi Hanji

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 17:34
CPC Classifications
C; C08; C08F; C08F10/00; C08F10/02; C08F210/00; C08F210/16; C08F110/00; C08F110/02; Y; Y10; Y10S; Y10S526/00; Y10S526/905

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 315 words
In a slurry polymerization process for producing an ethylene homopolymer or ethylene-α-olefin copolymer in multiple stages, in which the gas phase hydrogen concentration in each stage is different, by the use of a catalyst system comprising a transition metal compound component and an organoaluminum compound component, the improvement which comprises conducting the polymerization in a molar ratio, of gas phase hydrogen to ethylene, of 0.5 to 15 in the first stage thereby polymerizing 30 to 95% by weight of the overall polymerization amount and in the second stage in a molar ratio, of gas phase hydrogen to ethylene, not exceeding 0.2, by using as the transition metal compound component a solid catalyst component comprising a titanium compound and/or vanadium compound supported on a solid carrier obtained by the reaction of an organomagnesium compound and a halogenated aluminum compound and/or halogenated silicon compound represented by the general formula R'.sub.n AlX.sub.3-n and/or the general formula R.sup.2.sub.m SiX.sub.4-m wherein R' and R 2 are each an alkyl, cycloalkyl, aralkyl, aryl, or alkenyl group having up to 20 carbon atoms, X is a halogen atom, and n and m are numbers defined by 0≦n<3 and 0≦m<4, respectively; wherein the molar ratio of said organomagnesium compound to said halogenated aluminum compound and/or halogenated silicon compound is within the range of 0.1/1 to 10/1; wherein the amount of said titanium compound and/or vanadium compound supported on said solid carrier is 0.1 to 30% by weight in terms of titanium and/or vanadium atom based on the total amount of the supported compound and the carrier; wherein said reaction of the organomagnesium compound with the halogenated aluminum compound and/or halogenated silicon compound is carried out at 0° to 100° C.; and, wherein said organomagnesium compound is represented by the general formulae R.sup.3 MgX and/or R.sub.2.sup.3 Mg wherein R 3 is an alkyl, aralkyl, aryl, or alkenyl group having up to 20 carbon atoms.
Claim 2
Dependent Claim 315 words
In a slurry polymerization process for producing an ethylene homopolymer or ethylene-α-olefin copolymer in multiple stages, in which the gas phase hydrogen concentration in each stage is different, by the use of a catalyst system comprising a transition metal compound component and an organoaluminum compound component, the improvement which comprises conducting the polymerization in a molar ratio, of gas phase hydrogen to ethylene, of 0.5 to 15 in the first stage thereby polymerizing 30 to 95% by weight of the overall polymerization amount and in the second stage in a molar ratio, of gas phase hydrogen to ethylene, not exceeding 0.2, by using as the transition metal compound component a solid catalyst component comprising a titanium compound and/or vanadium compound supported on a solid carrier obtained by the reaction of an organomagnesium compound and a halogenated aluminum compound and/or halogenated silicon compound represented by the general formula R'.sub.n AlX.sub.3-n and/or the general formula R.sup.2.sub.m SiX.sub.4-m wherein R' and R 2 are each an alkyl, cycloalkyl, aralkyl, aryl, or alkenyl group having up to 20 carbon atoms, X is a halogen atom, and n and m are numbers defined by 0≦n<3 and 0≦m<4, respectively; wherein the molar ratio of said organomagnesium compound to said halogenated aluminum compound and/or halogenated silicon compound is within the range of 0.1/1 to 10/1; wherein the amount of said titanium compound and/or vanadium compound supported on said solid carrier is 0.1 to 30% by weight in terms of titanium and/or vanadium atom based on the total amount of the supported compound and the carrier; wherein said reaction of the organomagnesium compound with the halogenated aluminum compound and/or halogenated silicon compound is carried out at 0° to 100° C.; and, wherein said organomagnesium compound is represented by the general formulae R.sup.3 MgX and/or R.sub.2.sup.3 Mg wherein R 3 is an alkyl, aralkyl, aryl, or alkenyl group having up to 20 carbon atoms.
Claim 3
Dependent Claim 19 words
A process according to claim 1, wherein said solid carrier is formed in the presence of an ether solvent.
Claim 4
Dependent Claim 15 words
A process according to claim 1, wherein said halogenated aluminum compound is anhydrous aluminum chloride.
Claim 5
Dependent Claim 14 words
A process according to claim 1, wherein said halogenated silicon compound is silicon tetrachloride.
Claim 6
Dependent Claim 31 words
A process according to claim 1, wherein the molar ratio of said organomagnesium compound to said halogenated aluminum compound and/or halogenated silicon compound is within the range of 0.5/1 to 2.0/1.
Claim 7
Dependent Claim 46 words
A process according to claim 1, wherein the amount of said titanium compound and/or vanadium compound supported on said solid carrier is 0.1 to 15% by weight in terms of titanium and/or vanadium atom based on the total amount of the supported compound and the carrier.
Claim 8
Dependent Claim 24 words
A process according to claim 1, wherein said polymerization amount in the first stage is 40 to 85% by weight of overall polymerization amount.
Claim 9
Dependent Claim 24 words
A process according to claim 1, wherein the molar ratio of gaseous phase hydrogen to ethylene in the first stage is 1 to 10.
Claim 10
Dependent Claim 24 words
A process according to claim 1, wherein the molar ratio of gaseous phase hydrogen to ethylene in the second stage is 0.1 to 0.002.

References Cited (Backward Citations)

GB1057728A Cited
US3392213A Cited
GB1233599A Cited
US3592880A Cited
DE2104024A1 Cited
US4004071A Cited
US4223117A Cited
DE2826548A1 Cited
GB2020672B Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-10-04 1986-04-05 1986-10-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-10-04 1990-04-05 1990-10-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-10-04 1994-04-05 1994-10-05 $7700.00 Window Closed / Lapsed

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